Method for preparing biodiesel by biological-chemical catalytic coupling
A chemical catalysis and biodiesel technology, applied in biofuel, fat production, petroleum industry, etc., can solve the problems of lipase toxicity, excessive alcohol beard, deep color, etc., and achieve low cost, high product quality and light color effect
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example 1
[0018] Example 1: Using soybean salad oil as the raw material, using a stirring tank as the premix tank, feed 20kg soybean salad oil each time, add methanol in the theoretical molar ratio, 40L petroleum ether as a solvent, add 2kg water, and use a plunger pump to mix evenly The material is pumped into the fixed bed reactor. Each reaction column is filled with 1.5kg of immobilized lipase (enzyme activity is 20000U / g), and the three reaction columns are first-level reactions, divided into three-level reactions. The reaction temperature is 38℃, and the fatty acid methyl ester content is 82.4%-88.5 % Enzyme-catalyzed reaction solution, after removing the solvent, add methanol with twice the theoretical molar ratio of the remaining materials, 0.4Kg concentrated sulfuric acid, and react at 82°C for 3 hours to obtain an acid-catalyzed reaction solution with a fatty acid methyl ester content of 97.4%-99%. After rectification and separation, a biodiesel product is obtained.
example 2
[0019] Example 2: Using waste oil with an acid value of 125.5mgKOH / g as a raw material, using a stirring tank as a premix tank, feed 20kg waste oil each time, adding methanol with a theoretical molar ratio, 40L petroleum ether as a solvent, adding 2kg water, and using The plunger pump pumps the uniformly mixed materials into the fixed bed reactor. Each reaction column is filled with 1.5kg of immobilized lipase enzyme (enzyme activity is 20000U / g), and the three reaction columns are the first-level reaction, which is divided into three-stage reactions. The reaction temperature is 38℃, and the fatty acid methyl ester content is 81.4%- 86.5% of the enzyme-catalyzed reaction solution, after removing the solvent, add methanol with twice the theoretical molar ratio of the remaining materials, 0.6Kg of concentrated sulfuric acid, and react at 80°C for 3 hours to obtain an acid-catalyzed reaction solution with a fatty acid methyl ester content of 97.2%-98.8%. After rectification and se...
example 3
[0020] Example 3: Using acidified oil as the raw material, using a stirring tank as the premix tank, each time feed 10kg of acidified oil, add methanol with theoretical molar ratio, 20L petroleum ether as solvent, add 1kg of water, and use a plunger pump to mix the homogeneous materials Pump into the fixed bed reactor. Each reaction column is filled with 0.75kg of immobilized lipase (enzyme activity is 20000U / g), and the three reaction columns are the first-level reaction, which is divided into three-stage reactions. The reaction temperature is 38℃, and the fatty acid methyl ester content is 83.4%-88.2 % Of the enzyme-catalyzed reaction solution, after removing the solvent, add methanol with twice the theoretical molar ratio of the remaining materials, 0.4Kg concentrated phosphoric acid, and react at 90°C for 3h to obtain an acid-catalyzed reaction solution with a fatty acid methyl ester content of 98.1%-99%. After rectification and separation, a biodiesel product is obtained. ...
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